This is an author-deposited version published in : http://oatao.univ-toulouse.fr/
Eprints ID : 10260
To link to this article : DOI:10.1017/jfm.2011.475
URL :
http://dx.doi.org/10.1017/jfm.2011.475
To cite this version :
Magnaudet, Jacques
A 'reciprocal' theorem for the prediction of loads on a body moving in an inhomogeneous flow at arbitrary Reynolds number- CORRIGENDUM
.
(2011) Journal of FluidMechanics, vol. 689 . pp. 605-606. ISSN 0022-1120
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A ‘reciprocal’ theorem for the prediction of loads
on a body moving in an inhomogeneous flow at
arbitrary Reynolds number – CORRIGENDUM
Jacques Magnaudet
Institut de M´ecanique des Fluides de Toulouse, UMR CNRS/INPT/UPS 5502, All´ee Camille Soula, 31400 Toulouse, France
In Magnaudet (2011) an inertial contribution was overlooked during the derivation of (3.6). Indeed, when generalizing (E.5), which is valid for an irrotational velocity field ˜U = ∇ ˜Φ, to (E.6) which holds for any velocity ˜U, an extra term R
V( ˜U −∇ ˜Φ)·(∇UU+T∇UU)· ˆU dV arises on the right-hand side of the latter and hence on that of (E.8). Therefore the right-hand side of (3.6) actually involves an additional contribution −2 RV( ˜U − ∇ ˜Φ) · SU· ˆUdV, where SU=1/2(∇UU+T∇UU) denotes the strain-rate tensor associated with the undisturbed flow field. This contribution to the force and torque results from the distortion by the underlying strain rate of the vortical velocity disturbance ˜U − ∇ ˜Φ generated either by the dynamic boundary condition at the body surface SB (and possibly on the wall SW), or/and by the vorticity ωU of the undisturbed flow within the core of the fluid. This extra term gives in turn rise to an additional contribution −2 RV( ˜U0 −∇ ˜Φ0) · S0 · ˆUdV on the right-hand side of (3.13)–(3.15). This term was not present in the inviscid expressions established by Miloh (2003) because his derivation was restricted to situations in which the velocity disturbance is irrotational throughout the flow domain. This extra term does not alter the conclusions brought in the present paper for inviscid two-dimensional flows, nor those corresponding to the short-time limit of inviscid three-dimensional flows. In the limit Re → ∞ considered in the example of § 4.3, the disturbance is still irrotational outside the boundary layers that develop around the bubble and along the wall, respectively. The leading order in the vortical velocity disturbance is of O(Re−1/2) around the bubble, both in the ek and e⊥ directions. Near the wall, it is of O(κ2) (respectively O(κ2Re−1/2)) in the e
k (respectively e⊥) direction. Since the thickness of both boundary layers is of O(Re−1/2) and ˆU · e
⊥ grows linearly with the distance to the wall, the extra term −α RV{( ˜U0−∇ ˜Φ0) · e⊥( ˆU · ek) +( ˜U0−∇ ˜Φ0) · ek( ˆU · e⊥)} dV yields an O(αRe−1) net contribution provided by the bubble boundary layer and only an O(ακ2Re−1) correction provided by the wall boundary layer. Hence the inviscid predictions (4.26) and (4.33) are unchanged and there is an O(αRe−1) correction to the viscous drag and lift, similar in magnitude to that resulting from the term −R
V φω0ˆ ·( ˜ω + ˜ωB)0 dV. Owing to the weak inhomogeneity assumption invoked in §§ 3.2 and 4.3, the dimensionless shear rate α must be much smaller than unity for (4.26) and (4.33) to hold. Hence, in this context, the above corrections to the drag are much smaller than the leading, O(Re−1), contribution provided by the surface term
Re−1R
SB{( ˆU − ek) × ω} · n dS. Note that the above Re
−1 prefactor is missing on the right-hand side of (4.16) and (4.19).
R E F E R E N C E S
MAGNAUDET, J. 2011 A ‘reciprocal’ theorem for the prediction of loads on a body moving in an inhomogeneous flow at arbitrary Reynolds number. J. Fluid Mech. 689, 564–604.
MILOH, T. 2003 The motion of solids in inviscid uniform vortical fields. J. Fluid Mech. 479,